EP2196487A1 - Silicone polyether copolymer systems and method for production of same using alkoxylation reaction - Google Patents

Abstract

An alkoxylation of silicone-polyether copolymers comprises using double metal cyanide catalysts. An independent claim is included for the silicone-polyether copolymers prepared by above method.

Description

The invention relates to a process for the double metal cyanide-catalyzed alkoxylation of silicone polyether copolymers and their mixtures with polyetherols to high molecular weight, hydrophobic and hydrophilic structural elements having silicone polyether copolymer systems.

Silicone polyether copolymers represent a class of substances that is used in a variety of industrial applications, e.g. as surfactants, emulsifiers, wetting and dispersing additives, paint leveling agents, lubricants, as auxiliaries for tertiary mineral oil extraction, as textile auxiliaries for finishing fibers, yarns or flat textile products as defoamers, as cosmetic additives (emulsifiers) and as foam stabilizers, especially in polyurethane foam.

The polyether siloxanes are so versatile useful because you can influence their properties, in particular their hydrophilic / hydrophobic balance by a suitable choice of the siloxane block or siloxane blocks on the one hand and by suitable design of the polyether block or the polyether blocks and set to the desired value.

The siloxane block may be linear or branched, wherein the absolute number of di- and trifunctional siloxy units and their numerical ratio to each other in wide Limits are adjustable. It is also possible, in addition to polyoxyalkylene radicals, to bind other modifying groups to the Si atoms. Examples are long-chain hydrocarbon radicals, hydrocarbon radicals substituted by halogen atoms, cyano groups or polar radicals, hydroxyl groups, etc.

In the case of the silicone-polyether copolymers, a distinction is in principle made between SiOC- or SiC-linked systems. In the first case, the siloxane framework is connected to the polyether residues via SiOC bonds. In the second case, the siloxane moiety is linked to the polyether residues via SiC bonds.

The older route of the SiOC linkage makes use, for example, of the use of chlorosiloxanes which are reacted with polyether alcohols and often also with the use of amine auxiliary bases as hydrochloric acid scavengers to form polyethersiloxanes. An alternative approach to SiOC-based polyethersiloxanes opens up by the dehydrogenative reaction of SiH-group-carrying siloxanes (hydrogen siloxanes) with polyether alcohols in the presence of catalysts. As catalysts find eg acids, bases and metal complexes and also tris (pentafluorophenyl) borane use. Special linear polyethersiloxanes are accessible by direct alkoxylation of SiOH-bearing α, ω-dihydroxysiloxanes with epoxy monomers, as described in the not previously published document DE 10 2008 002713.8 is described.

Access to SiC-linked polyethersiloxane copolymers opens the hydrosilylation, ie, the mostly noble metal-catalyzed addition of SiH-group-containing siloxanes to unsaturated polyethers, for example to derivatives of vinyl or allyl alcohol. For the synthesis of the widespread allyl polyether-based copolymer systems, the unsaturated polyethers in a substantial stoichiometric excess of usually 20 to 40 mol% based on the SiH equivalents of the hydrogen siloxane used used to take into account the fact that, depending on the selected manufacturing path changing amounts of Propenylpolyether already contained in the allyl polyether and, in order to meet the unavoidable in the hydrosilylation allyl propenyl rearrangement, which makes a part of the allyl polyether used for the SiC linkage reaction useless. It should be noted that the terms polyether or polyetherol are partly synonymous in the literature and this application use, but clearly different from the silicone polyether copolymers.

As a consequence of this procedure contain the technically available, SiC-linked silicone polyether copolymers derived from allyl polyethers, not inconsiderable amounts of the isomerized excess polyether, which is indeed no longer hydrosilylatable with its β-double bond, but highly complexing to metals such eg acts on the platinum complexes often used in hydrosilylation.

The polyetherols, often referred to simply as polyethers, have long been known and are industrially produced in large quantities and serve, inter alia, by reaction with polyisocyanates as Starting compounds for the preparation of polyurethanes or else for the preparation of surfactants.

Most processes for the preparation of alkoxylation products (polyethers) use basic catalysts such as the alkali metal hydroxides and the alkali methylates. Especially widespread and known for many years is the use of KOH. Typically, a usually low molecular weight hydroxy-functional starter such as butanol, allyl alcohol, propylene glycol or glycerol is reacted in the presence of the alkaline catalyst with an alkylene oxide such as ethylene oxide, propylene oxide, butylene oxide or a mixture of different alkylene oxides to a polyoxyalkylene polyether. The strongly alkaline reaction conditions in this so-called living polymerization promote various side reactions. By rearrangement of propylene oxide in allyl alcohol, which in turn acts as a chain starter, and chain termination reactions arise polyether having a relatively broad molecular weight distribution and unsaturated by-products. In particular with allyl alcohol as starting alcohol, the alkoxylation reaction carried out under alkaline catalysis also produces propenyl polyethers. These propenyl polyethers prove to be unreactive byproducts in the case of the hydrosilylative further processing to give SiC-supported silicone polyether copolymers and are additionally-due to the hydrolytic lability of the vinyl ether bond contained in them and release of propionaldehyde-an undesirable source of olfactory product loadings. This is for example in the EP-A-1 431 331 described.

Among the disadvantages of the base-catalyzed alkoxylation is undoubtedly the need to free the reaction products obtained by means of a neutralization step of the active base. The distillative removal of the water formed during the neutralization and the separation of the salt formed by filtration are then absolutely necessary.
In addition to the base-catalyzed reaction, acidic catalysis for alkoxylation is also known. So will in DE 10 2004 007561 describe the use of HBF ₄ and of Lewis acids such as BF ₃ , AlCl ₃ and SnCl ₄ in alkoxylation technology.
Disadvantageous in the acid-catalyzed polyether synthesis proves the lack of regioselectivity in the ring opening unbalanced oxiranes such as propylene oxide, which means that polyoxyalkylene with partially secondary and primary OH termini are obtained in not clearly controlled manner. As in the case of the base-catalyzed alkoxylation reaction, a work-up sequence of neutralization, distillation and filtration is indispensable. If ethylene oxide is introduced as monomer into the acid-catalyzed polyether synthesis, the formation of dioxane as an undesired by-product can be expected.

As catalysts for the preparation of polyether alcohols, however, multimetal cyanide compounds or double metal cyanide catalysts, generally also referred to as DMC catalysts, are frequently used. Through the use of DMC catalysts, the content of unsaturated By-products are also minimized and, in comparison to the usual basic catalysts, the reaction proceeds with a significantly higher space-time yield. The preparation and use of double metal cyanide complexes as alkoxylation catalysts has been known since the 1960's and is described, for example, in US Pat US 3,427,256 . US 3,427,334 . US 3,427,335 . US 3,278,457 . US 3,278,458 . US 3,278,459 shown. Among those further developed in the following years and eg in US 5,470,813 and US 5,482,908 described, increasingly effective types of DMC catalysts are in particular zinc-cobalt hexacyanocomplexes. Owing to their extraordinarily high activity, only low catalyst concentrations are required for the preparation of polyetherols, so that the work-up stage required for conventional alkaline catalysts-consisting of the neutralization, the precipitation and the filtration of the catalyst-can be dispensed with at the end of the alkoxylation process. The alkoxylation products prepared with DMC catalysts are characterized by a much narrower molecular weight distribution compared to alkali-catalyzed products. The high selectivity of the DMC-catalyzed alkoxylation is due to the fact that, for example, propylene oxide-based polyethers contain only very small amounts of unsaturated by-products.

The alkoxylation reaction carried out in direct comparison with alkali and acid catalysis on DMC catalysts is so advantageous among the described technical features that it is suitable for the development of continuous processes for the preparation voluminous easier, mostly only from PO units existing, polyethers has led.

The EP 0 485 637 teaches a process for the preparation of polyoxyalkylene group-containing organopolysiloxanes which comprises subjecting organosiloxanes whose functional groups to alkylene oxides have active hydrogen atoms and fluorine compounds using alkylene oxides to undergo ring-opening polymerization on multimetal cyanide complexes. As a disadvantage of an acid-catalyzed preparation of the organopolysiloxanes is here found that homopolymers of alkylene oxides are formed as by-products, which would make it difficult to produce polyoxyalkylene compounds with high molecular weights.

The molecularly defined, pure organic fluorine compounds described in EP 0 485 637 are just as easy to alkoxylate as the organosiloxane derivatives claimed in the teaching, the functionality of which comprises active hydrogen groups of the type -OH, -SH, -NH ₂ , -NHR and -CO ₂ H attached to a C ₃ -C ₁₀ hydrocarbon radical optionally containing an ether, thioether or amino bridging. The organosiloxane starting materials which can be obtained, for example, via hydrosilylation are easy to purify, since the excess proportion of the low molecular weight alcohols, thio alcohols, amines and acids used in their preparation can be separated off very easily by distillation. In the EP 0 485 637 required hydrophobicity of the organosiloxane chain starter used on the one hand requires that they must be free of hydrophilic polyether excess fractions, and the other that their basic chemical structure is dominated by a hydrophobic, relatively long-chain Siloxangrundkörper to which SiC-linked short organic, not to be designated as a polyether, preferably OH-functional radicals having a maximum of 10 carbon atoms are attached. Such hydrophobic products are molecularly uniform and characterized in GPC analyzes by a single peak, monomodal.
Thus, they are not conventional surfactant polyethersiloxanes whose typical feature is that they represent technical, non-purified copolymers with long SiC-bonded terminal or pendant hydrophilic polyether chains and moreover contain other components such as hydrophilic unsaturated polyethers and their rearrangement products. In principle, it is an essential feature of the polyether siloxanes that they consist of a hydrophobic siloxane skeleton and a hydrophilic polyether moiety and represent complex chemical compositions, ie no defined pure substances. Thus, in surfactant applications, a balanced, preferably adjustable ratio between the hydrophobic (siloxane backbone) and hydrophilic (polyether substitution) residues is not only desired but required. In technical polyethersiloxanes not only the chemical structure of the polyether-siloxane copolymer determines the property profile, but quite decisively also the always present proportion of excess polyethers, which accounts for 20-40 wt .-% of the total product and gives the system an increased hydrophilicity. Practice teaches that the surface-active properties of such hydrosilylation products of the sum of all individual components, their chemical structure, their Molar mass and molecular weight distribution and their percentage in the overall system is determined. In GPC analyzes, the complexity of the products obtained by hydrosilylation, in contrast to those in EP 0 485 637 hydrophobic organosiloxanes, in the form of multimodal curves and very broad molecular weight distributions. Thus, GPC analyzes of typical technical polyethersiloxanes are characterized by at least two peak maxima or at least two peak groups that differ significantly in their molecular weight. The presence of free polyethers is manifested by one or more peaks in the low molecular weight range, often at molar masses of less than 5,000 g / mol. These proportions of mostly allyl alcohol-based excess polyethers represent relatively hydrophilic components in the overall system. The GPC maxima in the relatively high molecular weight range up to 100,000 g / mol or even more are based on polysiloxane-polyether copolymers. They are the major components in many reaction mixtures after hydrosilylation and are often included at 60-80% by weight. They contain in their structure both a hydrophobic siloxane base and one or more hydrophilic polyether chains, linked chemically via SiC bonds, in one molecule.
The application properties of these hydrophobic and hydrophilic structural elements having substance mixtures are crucially determined by their chemical composition and the chemical structure of all individual components. The composition of the polyethersiloxanes in turn is directly linked to the process principle of hydrosilylation. Virtually all reaction products in the noble metal-catalyzed addition of eg allyl polyethers Hydrogen siloxanes during hydrosilylation, including rearrangement or unreacted starting materials, form part of the final product. The flexibility in the targeted development of polyethersiloxanes are thus limited, which are in the chemistry of the hydrosilylation process.

Thus, polyether siloxanes with very long-chain polyethers are difficult or even impossible to prepare, since the rate of hydrolysis with hydrosilylation decreases with increasing chain length of the polyether and no quantitative SiH conversion is possible or the amount of catalyst and reaction time must be increased so much that the production is uneconomical.

With regard to their chain length, their molecular weight distribution and monomer sequence, the polyether chains connected terminally or laterally to the respective siloxane skeleton are always identical to the excess polyethers. For given educts, only the mixing ratio of excess polyethers to silicone polyethers can be influenced by the hydrosilylation conditions. In GPC analyzes, this manifests itself in the fact that the position of the peaks along the molar mass axis is virtually invariable when the starting materials to be hydrosilylated-hydrogen siloxane and polyethers-are given.

It is not possible according to the current state of the art to produce polyethersiloxane systems in which the free excess polyether portion is structurally linked to the SiC Polyether portion of the copolymer is different.

Surprisingly, it has now been found that even complex, hydrophobic and hydrophilic structural elements having technical silicone polyether copolymers can be used as chain starters for alkoxylation reactions. This result is surprising to those skilled in the art, because these substances are distinguished not only by a significantly lower density of active hydrogen atoms, but also of lesser purity than the starter commonly used. Such highly functionalized polyethersiloxanes are obtained in part by a common hydrosilylation of hydrogen siloxanes with mixtures of different high molecular weight polyethers, resulting in extremely broad molecular weight distributions and multimodal GPC curves in such cases. The chemical composition of the polyether siloxanes used according to the invention as chain starters for the alkoxylation is therefore very complex. In addition, these copolymers contain by-products and catalyst residues from the hydrosilylation, which can not be separated. These by-products and especially catalyst residues represent potential catalyst poisons in the context of the alkoxylation according to the invention by means of DMC catalysts.
Polyether siloxanes can not be selectively alkoxylated to extended chain products by the conventional route of alkaline or acid catalysis. The strongly basic or acidic reaction conditions and the use of water in the subsequent neutralization and workup stage inevitably lead to Rearrangements and a hardly controllable reorganization of the siloxane body.

On the other hand, under the approximately neutral and anhydrous reaction conditions of the DMC-catalyzed alkoxylation, it is also possible to use hydrolysis-sensitive compounds such as silanols or OH-functional silicone polyethers carrying SiOH groups to start the siloxane backbone as starters for the synthesis of relatively high molecular weight silicone polyether copolymers. According to previous doctrine, the process of DMC catalysis has a decisive limitation when mixtures of substances of complex composition consisting of epoxide-reactive species of greatly differing chain lengths are to be alkoxylated in the mixture. The person skilled in the art is familiar from the term "catch-up kinetics" in that, unlike conventional basic or acidic catalysis, the reactivity toward the alkylene oxide addition is highly dependent on the molecular weight of the OH-functional starting compounds. Thus, it is known that low molecular weight chains are much more reactive than higher molecular weight chains. The preference for low molecular weight species is so pronounced that according to previous knowledge in the Alkylenoxiddosage the or the epoxy monomers add to the almost only each short-chain reactive components in the respective reaction mixture. The uneven alkylene oxide addition known from DMC catalysis thus leads to unequal chain growth.
Against the background of the considerable molar mass differences when using technical polyethersiloxanes as chain starter - free polyethers with average molecular weights of mostly <4,000 g / mol exist in addition to silicone polyethers usually with 10,000-50,000 g / mol - would therefore be expected that in the DMC-catalyzed alkoxylation almost all alkylene oxide is added to the very low molecular weight free polyether.

All the more surprising therefore was the discovery that even technical silicone polyether copolymers are accessible to double metal cyanide catalysts of a ring-opening alkoxylation reaction, wherein both the polyethersiloxane copolymers and the free polyether moieties, regardless of their so different hydrophilicity or hydrophobicity and molecular weights, function as OH-functional chain starters , This result is completely unexpected for the skilled person because it contradicts the common view of the generality of "catch-up kinetics" in DMC catalysts.

Silicone polyether copolymers for the purposes of this invention are those which contain at least 5 repeat units of the ether fragment (characterized by the subscript e in formula (Ia) in the polyether part) and / or have an average molecular weight of the polyether fragment of at least 220 g / mol.

Especially surprising and unpredictable is the special and unusual kinetics with which the DMC-catalyzed addition of alkylene oxides to the different OH-functional compounds of the complex starting mixture takes place. With a characteristic speed for the respective system, the chain length of the free excess polyethers increases in the course of the alkylene oxide feed also the chain length of the bound to the siloxane polyether strands. This contradicts the so-called "catch-up kinetics" known to the person skilled in the art from the DMC-based alkoxylation of, for example, alcohols or polyetherols, and which, for example, US Pat EP 1 942 126 A1 The basic statement that almost exclusively the more reactive short-chain species react in a mixture of different high molecular weight OH-functional starters. Double metal cyanide catalysts according to EP 1 942 126 A1 in principle a pronounced preference for the respective low-molecular weight hydroxyl-bearing components in a mixture of reactive species.

Surprisingly, it has now been found that in the case of the DMC-catalyzed alkoxylation, the alkylene oxides in no way predominantly add to the low molecular weight excess free polyethers but also to the much higher molecular weight polyethersiloxanes bearing reactive OH groups. This results in hydrophobic and hydrophilic structural elements having, silicone polyether copolymers and polyether-containing mixtures with previously unreachable new composition.

From GPC analyzes like in Fig. 1 As shown in Example 5, it is clear that all OH-bearing components of the polyethersiloxane participate in the alkoxylation reaction. However, because the chain length of the siloxane-bound polyether segments grows at a rate different from that of the free excess polyethers, new polyethersiloxane systems are formed. The characteristic chain growth of the reactive species is evident in GPC analyzes in the form of the relative shift of the peaks along the molecular weight axis.
Fig. 1 (Example 5) shows the typical for the inventive process chain growth of all OH-functional components of a polyether siloxane in the stepwise addition of propylene oxide. The chainstarter in Fig. 1 is a polyethersiloxane prepared beforehand by hydrosilylation of a hydrogen siloxane of formula (I) having the structure m ¹ = 42, m ² = 6, m ³ = m ⁴ = 0, X = X ¹ = methyl with a 35val% excess (Based on the SiH groups) of an OH-terminated allyl polyether of average molecular weight 600 g / mol and consisting of 50 wt .-% of ethylene oxide and 50 wt .-% of propylene oxide units, prepared according to the prior art. The GPC analysis of this starter is characterized by two peak maxima at about 600 g / mol for the free polyether portion and at about 9,000 g / mol for the polyethersiloxane. After feeding a first portion of propylene oxide according to the inventive method, both peak maxima shift to higher molecular weights. A product 1 is obtained in which the free polyether has grown to an average molecular weight of about 2,700 g / mol, the silicone polyether copolymer to a maximum at about 18,000 g / mol. Further addition of propylene oxide continues the trend and general chain growth of all reactive species in the system. Product 2 contains the extended to a mean molecular weight of about 13,000 g / mol of free polyether and a silicone polyether copolymer peak peak at 22,000 g / mol and very high molecular weight copolymer contents of more than 100,000 g / mol.

The process according to the invention makes it possible for the first time to fundamentally modify a silicone polyether obtained by a conventional method by a subsequent alkoxylation reaction and to obtain the siloxane skeleton.
Thus, there is provided a process for the alkoxylation of silicone polyether copolymers wherein double metal cyanide catalysts are used.
Thus, for example, polysiloxane-polyether copolymer systems with much longer, possibly functionalized polyether chains can be synthesized. In addition, the mass ratio of free excess polyethers to silicone polyether copolymers can be varied compared to the starting copolymer. In the same way, the chemical structure of the optionally free or bonded to the siloxane polyether can be varied and so for example, the average molecular weight of the silicone polyether copolymer in relation to the average molecular weight of the polyether excess control.
Thus, in the process of the present invention, compositions are alkoxylated on double metal cyanide catalysts containing silicone polyether copolymers to form silicone polyether copolymer compositions having increased average molecular weight over the starting materials.
In the process according to the invention, preference is given to alkoxylation of silicone polyether copolymers in compositions containing free polyetherols to double metal cyanide catalysts, wherein the structure of the average molecular weight of the silicone polyether copolymer used in admixture with free polyetherol is at least at the same rate as the structure of Molar mass of the free polyetherol present in the educt mixture.

The preferred alkoxylation of the silicone polyether copolymers in compositions containing free polyetherols shows that the buildup of the average molecular weight of the silicone polyether copolymer used in admixture with free polyetherol is at least as likely to occur as the molecular weight of the free polyetherol present in the reactant mixture. The structure of the silicone polyether copolymers is usually faster than the structure of the molecular weight of the polyetherol.

The rate of alkoxylation according to the invention is greater than or equal to the rate of alkoxylation of the polyetherol for all of the silicone polyether copolymers participating in the reaction.

The new process creates new possibilities for adjusting the hydrophilic / hydrophobic ratio and thus completely new scope for the development of surfactants.

A particular advantage of the process according to the invention is also the great robustness of the alkoxylation process, with which new, high molecular weight and highly functionalized polyethersiloxanes are made accessible. The alkoxylated silicone polyether copolymers can thus have higher molecular weight, complex and highly functionalized, hydrophobic and hydrophilic structural elements.

The method claimed according to the invention makes it possible to react SiC-linked polyethersiloxanes of very different structure, molecular weight and molecular weight distribution which have at least one reactive carbon-bonded hydroxyl group in the presence of a DMC catalyst with epoxide monomers and optionally further monomers by optionally ring-opening alkoxylation reaction to give chain-extended, modified polyethersiloxanes ,

With the method according to the invention, it is possible to address an elementary basic need in the chemistry of higher molecular weight SiC-based silicone polyether copolymers. With increasing chain length and concomitantly increasing molecular weight, allyl polyethers greatly lose reactivity in the hydrosilylation reaction as compared to corresponding short chain polyethers. As a result, the reaction rate decreases and the achievement of quantitative SiH conversion becomes considerably difficult or even impossible. The access to polyether siloxanes with higher molecular weight polyether components is therefore by no means given via the customary addition to siloxanes containing SiH groups.

A process is thus provided for the preparation of polyethersiloxanes-containing alkoxylation products by means of DMC catalysis in which one or more epoxide-functional monomers of the formula (II) individually or in admixture with other epoxide compounds of the formula (III) and optionally further comonomers such as lactones ( IV), cyclic anhydrides (V), (VI), carbon dioxide or oxetanes optionally blockwise or random to a Organosiloxane chain starters of the formulas (I) or (VII) are added with at least one reactive hydrogen.
Another object of the process of the present invention is to obtain the advantages of high rate reaction and catalyst deactivation and separation known from the double metal cyanide systems and to preserve the hydrolysis-sensitive siloxane backbone under the conditions of selective DMC-catalyzed alkoxylation.

wobei

m¹

eine ganze Zahl von 0 bis 500, vorzugsweise von 10 bis 200, insbesondere 15 bis 100,

m²

eine ganze Zahl von 0 bis 60, vorzugsweise von 0 bis 30, insbesondere von 0 bis 25,

m³

eine ganze Zahl von 0 bis 60, vorzugsweise von 0 bis 30, insbesondere von 0 bis 25,

m⁴

eine ganze Zahl von 0 bis 10, vorzugsweise von 0 bis 3, ist,

X

ein linearer, cyclischer oder verzweigter, aliphatischer oder aromatischer, gesättigter oder ungesättigter Kohlenwasserstoffrest mit 1 bis 20 C-Atomen ist, der ggfs. Heteroatome wie Sauerstoff, Stickstoff, Phosphor oder Schwefel enthalten kann, der jedoch vorzugsweise eine Methylgruppe ist,

X¹

wahlweise X, X² oder X³ ist,

X²

ein OH-funktioneller, ggfs. Ester- oder Carbonat-modifizierter Polyoxyalkylenrest der Formel (Ia) ist,

X³

ein endständig veretherter Polyoxyalkylenrest der Formel (Ib)

oder ein mit einer monofunktionellen Carbonsäure endständig veresterter Polyoxyalkylenrest der Formel (Ic) ist,

wobei

R⁴

einem linearen oder verzweigten Alkylrest von 1 bis 24 Kohlenstoffatomen, der an einen aromatischen oder cycloaliphatischen Rest gebunden ist, entspricht,

R⁷ und R⁸

unabhängig voneinander entweder Wasserstoff, Alkyl-, Alkoxy-, Aryl- oder Aralkylgruppen sind,

R⁹, R¹⁰, R¹¹ und R¹²

sind unabhängig voneinander entweder Wasserstoff, Alkyl-, Alkenyl-, Alkoxy-, Aryl- oder Aralkylgruppen. Der Kohlenwasserstoffrest kann cycloaliphatisch oder aromatisch über das Fragment Z verbrückt sein, wobei Z sowohl einen divalenten Alkylen- als auch Alkenylenrest darstellen kann,

R¹³

ist wahlweise eine Alkylgruppe mit 1 bis 18 C-Atomen, vorzugsweise Methyl,

R¹⁴

ist ein gesättigter oder ein ein- oder mehrfach ungesättigter, entweder linearer oder verzweigter, aliphatischer oder aromatischer Kohlenwasserstoffrest mit 1-30 Kohlenstoffatomen, der seinerseits OH-Gruppen tragen kann, und der vorzugsweise ein Methylrest ist, und wobei

c

eine ganze Zahl von 0 bis 24, vorzugsweise von 0 bis 12, besonders bevorzugt von 0 bis 8, ganz besonders bevorzugt von 0 bis 4 ist,

e

eine ganze Zahl von größer als 5, bevorzugt 6 bis 500, besonders bevorzugt 6 bis 300 und insbesondere 6 bis 200 ist und

f, g, h, i und j

ganze Zahlen von 0 bis 500, bevorzugt 0 bis 300, besonders bevorzugt 0 bis 200, insbesondere 0 bis 100 sind.

Starting compounds in the context of the process according to the invention are at least one polyethersiloxanes of the formula (I) which carry OH groups.

in which

m ¹

an integer from 0 to 500, preferably from 10 to 200, in particular 15 to 100,

m ²

an integer from 0 to 60, preferably from 0 to 30, in particular from 0 to 25,

m ³

an integer from 0 to 60, preferably from 0 to 30, in particular from 0 to 25,

m ⁴

is an integer from 0 to 10, preferably from 0 to 3,

X

is a linear, cyclic or branched, aliphatic or aromatic, saturated or unsaturated hydrocarbon radical having 1 to 20 C atoms, which may optionally contain heteroatoms such as oxygen, nitrogen, phosphorus or sulfur, but which is preferably a methyl group,

X ¹

optionally, X, X ² or X ^3,

X ²

is an OH-functional, optionally ester or carbonate-modified polyoxyalkylene radical of the formula (Ia),

X ³

a terminally etherified polyoxyalkylene radical of the formula (Ib)

or is a terminally esterified with a monofunctional carboxylic acid polyoxyalkylene radical of the formula (Ic),

in which

R ⁴

a linear or branched alkyl radical of 1 to 24 carbon atoms which is bonded to an aromatic or cycloaliphatic radical,

R ⁷ and R ⁸

independently of one another are either hydrogen, alkyl, alkoxy, aryl or aralkyl groups,

R ⁹ , R ¹⁰ , R ¹¹ and R ¹²

independently of one another are either hydrogen, alkyl, alkenyl, alkoxy, aryl or aralkyl groups. The hydrocarbon radical can be cycloaliphatic or aromatic via the fragment Z be bridged, where Z may represent both a divalent alkylene and alkenylene,

R ¹³

is optionally an alkyl group having 1 to 18 carbon atoms, preferably methyl,

R ¹⁴

is a saturated or a mono- or polyunsaturated, either linear or branched, aliphatic or aromatic hydrocarbon radical having 1-30 carbon atoms, which in turn can carry OH groups, and which is preferably a methyl radical, and wherein

c

is an integer from 0 to 24, preferably from 0 to 12, more preferably from 0 to 8, most preferably from 0 to 4,

e

an integer greater than 5, preferably 6 to 500, more preferably 6 to 300 and especially 6 to 200, and

f, g, h, i and j

integers from 0 to 500, preferably 0 to 300, particularly preferably 0 to 200, in particular 0 to 100 are.

The polyethersiloxanes described by formula (I) include the proportions of free excess polyethers contained in the process.

The various monomer units within the siloxane chain or within the associated polyether chain can be constructed with each other optionally blockwise or random. The index numbers given in the formulas given herein and the ranges of values of the indicated indices are to be understood as the mean values of the possible statistical distribution of the actual isolated structures and / or their Mixtures. This also applies to structural formulas which are exactly reproduced as such.

SiC-linked polyethersiloxanes of the formula (I) are prepared industrially by noble metal-catalyzed hydrosilylation reactions of the corresponding hydrogensiloxanes with terminally unsaturated, for example allyl alcohol-based, polyethers. Such polyethers are prepared in a separate prior alkoxylation process of the prior art by alkoxylation of allyl alcohol with alkylene oxides and possibly additional comonomers whereby ester or carbonate groups can be incorporated into the polyether backbone. The free fractions of excess polyethers present as by-products in the technical polyethersiloxanes (I) do not affect the DMC-catalyzed alkoxylation reaction according to the invention. If these excess polyethers are OH-functional, they likewise function as chain starters for the reaction with epoxide monomers in the context of the alkoxylation process.

In addition to the SiC-linked polyethersiloxanes of the formula (I), it is also possible to use linear polyethersiloxanes which are chain-terminated OH-functional SiOCs and are obtainable by direct alkoxylation of α, ω-dihydroxysiloxanes carrying SiOH groups with epoxide monomers and their preparation in the non-prepublished publication DE 10 2008 002713.8 is described as being used as a chain starter. With respect to these chain starters, the disclosure content of DE 10 2008 002713.8 to be considered in full as part of the disclosure of this application.

wobei X¹ in mindestens einem Fall pro Molekül dem OH-funktionellen organischen Rest X² entspricht. Die durch Formel (VII) beschriebenen cyclischen Copolymere schließen die prozessbedingt enthaltenen Anteile an freien Überschusspolyethern mit ein.In addition, hydroxyl-bearing organosiloxanes having a cyclic structure of the formula (VII) are also suitable as starters for the DMC-catalyzed alkoxylation according to the invention,

where X ¹ corresponds in at least one case per molecule to the OH-functional organic radical X ² . The cyclic copolymers described by formula (VII) include the proportions of free excess polyethers contained in the process.

mit R² oder R³, sowie R⁵ oder R⁶ gleich oder auch unabhängig voneinander H oder ein gesättigter oder gegebenenfalls einfach oder mehrfach ungesättigter, auch weiter substituierter, gegebenenfalls ein- oder mehrwertiger Kohlenwasserstoffrest, wobei für die Reste R⁵ oder R⁶ gilt, dass sie gleich einem einwertigen Kohlenwasserstoffrest sind. Der Kohlenwasserstoffrest kann cycloaliphatisch über das Fragment Y verbrückt sein; Y kann nicht vorhanden sein, oder aber eine Methylenbrücke mit 1 oder 2 Methyleneinheiten sein, ist Y gleich 0, so sind R² oder R³ unabhängig voneinander gleich ein linearer oder verzweigter Rest mit 1 bis 20, bevorzugt 1 bis 10 Kohlenstoffatomen, besonders bevorzugt ein Methyl-, Ethyl-, Propyl- oder Butyl-, Vinyl-, Allylrest oder Phenylrest. Vorzugsweise ist zumindest einer der beiden Reste in Formel (II) R² oder R³ Wasserstoff. Besonders bevorzugt werden als Alkylenoxide Ethylenoxid, Propylenoxid, 1,2-oder 2,3-Butylenoxid, Isobutylenoxid, 1,2-Dodecenoxid, Styroloxid, Cyclohexenoxid (hier ist R²-R³ eine -CH₂CH₂CH₂CH₂-Gruppe, Y damit -CH₂CH₂-) oder Vinylcyclohexenoxid oder deren Mischungen eingesetzt. Die Kohlenwasserstoffreste R² und R³ gemäß Formel (II) können ihrerseits weiter substituiert sein und funktionelle Gruppen wie Halogene, Hydroxylgruppen oder Glycidyloxypropylgruppen tragen. Zu solchen Alkylenoxiden gehören Epichlorhydrin und 2,3-Epoxy-1-propanol. Auch Gemische von Epoxiden der Formel (II) können eingesetzt werden, und zwar beliebig blockartig oder gemischt.As epoxy monomers, alkylene oxides of the general formula (II) can be used,

with R ² or R ³ , and R ⁵ or R ^{6 is the} same or independently H or a saturated or optionally mono- or polyunsaturated, also further substituted, optionally mono- or polyvalent hydrocarbon radical, where R ⁵ or R ⁶ applies in that they are equal to a monovalent hydrocarbon radical. The hydrocarbon radical may be cycloaliphatically bridged via the fragment Y; Y may not be present, or a methylene bridge with 1 or 2 methylene units, Y is 0, then R ² or R ^{3 are} independently a linear or branched radical having 1 to 20, preferably 1 to 10 carbon atoms, particularly preferred a methyl, ethyl, propyl or butyl, vinyl, allyl or phenyl radical. Preferably, at least one of the two radicals in formula (II) R ² or R ^{3 is} hydrogen. Particularly preferred alkylene oxides are ethylene oxide, propylene oxide, 1,2- or 2,3-butylene oxide, isobutylene oxide, 1,2-dodecene oxide, styrene oxide, cyclohexene oxide (in which R ² -R ^{3 is} -CH ₂ CH ₂ CH ₂ CH ₂ - Group, Y so that -CH ₂ CH ₂ -) or vinylcyclohexene oxide or mixtures thereof. The hydrocarbon radicals R ² and R ³ according to formula (II) may in turn be further substituted and bear functional groups such as halogens, hydroxyl groups or glycidyloxypropyl groups. Such alkylene oxides include epichlorohydrin and 2,3-epoxy-1-propanol. It is also possible to use mixtures of epoxides of the formula (II), in any desired block or mixed form.

bei denen mindestens eine Glycidyloxypropyl-Gruppe über eine Ether- oder Esterfunktion an einen Rest R⁴, der ein linearer oder verzweigten Alkylrest von 1 bis 24 Kohlenstoffatomen oder ein aromatischer oder cycloaliphatischer Rest sein kann, gebunden ist, in Kombination mit den in Formel (II) dargestellten Alkylenoxiden verwendet werden. Zu dieser Klasse von Verbindungen gehören zum Beispiel Allyl-, Butyl-, 2-Ethylhexyl-, Cyclohexyl-, Benzyl-, C₁₂/C₁₄-Fettalkohol-, Phenyl, p-tert.-Butylphenyl- oder o-Kresylglycidylether. Bevorzugt eingesetzte Glycidylester sind zum Beispiel Glycidylmethacrylat, Glycidylacrylat oder Neodecansäureglycidylester. Ebenso einsetzbar sind polyfunktionelle Epoxidverbindungen wie zum Beispiel 1,2-Ethyl-, 1,4-Butyl- oder 1,6-Hexyldiglycidylether.Also, glycidyl compounds such as glycidyl ethers and / or glycidyl esters of general formula (III),

in which at least one glycidyloxypropyl group is bonded via an ether or ester function to a radical R ⁴ which may be a linear or branched alkyl radical of 1 to 24 carbon atoms or an aromatic or cycloaliphatic radical, in combination with the radicals represented in formula (II ) alkylene oxides are used. This class of compounds includes, for example, allyl, butyl, 2-ethylhexyl, cyclohexyl, benzyl, C ₁₂ / C ₁₄ fatty alcohol, phenyl, p-tert-butylphenyl or o-cresyl glycidyl ether. Preferred glycidyl esters are, for example, glycidyl methacrylate, glycidyl acrylate or glycidyl neodecanoate. Likewise usable are polyfunctional epoxide compounds such as, for example, 1,2-ethyl, 1,4-butyl or 1,6-hexyl diglycidyl ether.

wobei n eine ganze Zahl von 2 bis 8 ist und R⁷ und R⁸ unabhängig voneinander entweder Wasserstoff, Alkyl-, Alkoxy-, Aryl- oder Aralkylgruppen darstellen. Als geeignete Lactone können in dem Zusammenhang beispielsweise ε-Caprolacton, δ-Valerolacton und γ-Butyrolacton sowie Gemische verschiedener Lactone verwendet werden. Bevorzugt ist die Verwendung von ε-Caprolacton als Comonomer. Während des Alkoxylierungsprozesses können die jeweiligen Epoxid- und Lactonmonomere in beliebiger Reihenfolge und variabler Menge nacheinander oder zeitlich parallel zu Polyetherestern mit blockartiger oder statistisch verteilter Sequenz der einzelnen Monomerbausteine copolymerisiert werden.The alkylene oxides of the formula (II) which can be used according to the invention can also be mixed with lactones of the formula (IV) under the conditions of the DMC-catalyzed alkoxylation, if appropriate in combination with other epoxides of the formula (III)

wherein n is an integer from 2 to 8 and R ⁷ and R ⁸ independently represent either hydrogen, alkyl, alkoxy, aryl or aralkyl groups. Suitable lactones in the context, for example, ε-caprolactone, δ-valerolactone and γ-butyrolactone and mixtures of different lactones can be used. Preference is given to the use of ε-caprolactone as comonomer. During the alkoxylation process, the respective epoxide and Lactonmonomere can be copolymerized in any order and variable amount sequentially or in parallel with polyether esters having a block or random sequence of the individual monomer building blocks.

wobei R⁹, R¹⁰, R¹¹ und R¹² unabhängig voneinander entweder Wasserstoff, Alkyl-, Alkenyl-, Alkoxy-, Aryl- oder Aralkylgruppen darstellen. Der Kohlenwasserstoffrest kann cycloaliphatisch oder aromatisch über das Fragment Z verbrückt sein, wobei Z sowohl einen divalenten Alkylenals auch Alkenylenrest darstellen kann. Bevorzugt eingesetzte cyclische Anhydride sind Bernsteinsäureanhydrid, Oct(en)yl-, Dec(en)yl- und Dodec (en) ylbernsteinsäueanhydrid, Maleinsäureanhydrid, Phthalsäureanhydrid, Hexahydro-, Tetrahydro-, Dihydro-, Methylhexahydro- und Methyltetrahydrophthalsäureanhydrid. Während des Alkoxylierungsprozesses können die jeweiligen Anhydridmonomere in beliebiger Reihenfolge und variabler Menge nacheinander oder zeitlich parallel zum Epoxidfeed unter Ringöffnung zu Polyetherestern copolymerisiert werden. Auch Mischungen von Anhydriden gemäß Formel (V) und (VI) sind einsetzbar.Alternatively or in addition to lactones, it is also possible to use saturated, unsaturated or aromatic cyclic dicarboxylic anhydrides according to the formulas (V) and (VI) as comonomers in addition to the epoxides of the formula (II) which can be used according to the invention and optionally further epoxides of the formula (III) under the conditions of the DMC catalyzed alkoxylation can be used,

wherein R ⁹ , R ¹⁰ , R ¹¹ and R ¹² independently represent either hydrogen, alkyl, alkenyl, alkoxy, aryl or aralkyl groups. The hydrocarbon radical may be bridged cycloaliphatically or aromatically via the fragment Z, where Z may be both a divalent alkylene and alkenylene radical. Preferred cyclic anhydrides are succinic anhydride, oct (en) yl, dec (en) yl and dodec (en) ylsuccinic anhydride, maleic anhydride, phthalic anhydride, hexahydro-, tetrahydro-, dihydro-, methylhexahydro- and methyltetrahydrophthalic anhydride. During the alkoxylation process, the respective anhydride monomers in any order and variable amount one after the other or temporally parallel to Epoxidfeed with ring opening to polyether esters are copolymerized. It is also possible to use mixtures of anhydrides of the formula (V) and (VI).

If the alkoxylation of polyethersiloxanes of the formula (I) is carried out in the presence of carbon dioxide, it is possible to prepare carbonate-modified polyethers or polyetheresters by insertion of carbon dioxide into the polymer chain. Such reactions preferably take place in autoclave reactors under pressure and carbon dioxide atmosphere. The carbonate content is variable and controllable, for example, by the choice of the temperature and pressure conditions during the reaction.

To start the alkoxylation reaction by the process according to the invention is the starting mixture consisting of one or more OH-functional starting compounds of the formulas (I) or (VII) or in the non-prepublished document DE 10 2008 002713.8 described polyether siloxanes and the double metal cyanide catalyst, which was optionally slurried previously suspended in a suspending agent in the reactor. As suspending agent, either a polyether, a polyethersiloxane or inert solvents can be used or, advantageously, one or more of the abovementioned starting compounds, or alternatively a mixture of the abovementioned components. At least one of the epoxide compounds according to formula (II) or (III) is added to the initially introduced starting mixture. To start the alkoxylation reaction and to activate the double metal cyanide catalyst is usually only a portion of the total amount of epoxide to be metered added. The molar ratio of epoxide to the reactive groups of the initiator, in particular the OH groups in the starting mixture, in the starting phase is preferably 0.1 to 300 to 1, preferably 0.2 to 200 to 1, in particular 0.4 to 100 to 1. It may be advantageous if, prior to the addition of the epoxide optionally present, the reaction inhibiting substances are removed from the reaction mixture, for example by distillation.

Starting the exothermic reaction may e.g. be detected by a pressure and / or temperature monitoring. A sudden drop in pressure in the reactor indicates, in the case of gaseous alkylene oxides, that the alkylene oxide is incorporated, thus initiating the reaction and reaching the end of the start-up phase.

After the initialization of the reaction, depending on the desired molecular weight, either further starting compound and further epoxide or only further epoxide are added at the same time. Alternatively, any mixture of different epoxides of formulas (II) and (III) can also be added. The epoxide monomers according to the formulas (II) or (III) can be added successively in any order. The reaction may e.g. for the purpose of reducing the viscosity of the reaction mixture in an inert solvent. Suitable inert solvents are hydrocarbons, in particular toluene, xylene or cyclohexane.

The molar ratio of the sum of the dosed epoxides, including the epoxides already added in the start phase, based on the starting compound used, In particular, based on the number of OH groups of the starting compound used, is preferably 1 to 10 ⁵ to 1, in particular 1 to 10 ⁴ to 1.

The addition of the epoxy compounds is preferably carried out at a temperature of 60 to 250 ° C, more preferably at a temperature of 90 to 160 ° C. The pressure is preferably 0.02 bar to 100 bar, more preferably 0.05 to 20 bar and in particular from 0.2 to 2 bar absolute. By carrying out the alkoxylation under reduced pressure, the reaction can be carried out very safely. Optionally, the alkoxylation may be carried out in the presence of an inert gas (e.g., nitrogen) or, in the presence of carbon dioxide, to produce polyethercarbonates, even at an overpressure of preferably 1 to 20 bars absolute.

The lactones (IV) or cyclic anhydrides (V) and (VI) which can be used for the preparation of ester-modified polyethersiloxanes can be added to the starter / catalyst mixture both in the start phase and at a later time in parallel to the epoxide dosage. The comonomers mentioned can also be metered in succession alternately with epoxides in the reactor.
The molar ratio of the epoxide monomers to cyclic anhydrides is variable. Usually, at least equimolar amounts of epoxide monomers based on anhydrides are used. Preferred is the use of the epoxides in a molar excess to ensure complete anhydride conversion. Lactones may optionally be in the stoichiometric during the alkoxylation Inadequate or excess based on the epoxy monomers are added.

For the preparation of carbonate-modified polyethersiloxanes the alkoxylation takes place in the presence of either gaseous or fed as dry ice solid carbon dioxide. Preferably, carbon dioxide gas is used, which can be supplied to the system of starter and DMC catalyst both before the start of the reaction, ie already during the initialization stage, and during the subsequent phase of the feed of epoxide monomers and possibly further comonomers. In order to increase the carbonate content in the end product, it is advantageous, according to the carbon dioxide consumption, recognizable by the decrease in pressure in the autoclave, to meter in further carbon dioxide continuously or in portions during the course of the reaction. The reaction preferably takes place at pressures of less than 100 bar, particularly preferably less than 20 bar.

After monomer addition and eventual post-reaction to complete the monomer conversion, any residues of unreacted monomer and possibly other volatile constituents are removed, usually by vacuum distillation, gas stripping or other methods of deodorization. The removal of volatile secondary components can be carried out either batchwise or continuously. In the case of the method based on DMC catalysis according to the invention, it is normally possible to dispense with filtration.

The process steps can be carried out at identical or different temperatures. The mixture of starter substance, DMC catalyst and, if appropriate, suspending agent initially introduced in the reactor in order to start the reaction can, before starting the monomer metering according to the teaching of US Pat WO 98/52689 be pretreated by stripping. In this case, an inert gas is added to the reaction mixture via the reactor feed and by means of a vacuum system connected to the reactor system, more volatile components are removed by applying a reduced pressure from the reaction mixture. In this simple way can from the reaction mixture substances which can inhibit the catalyst, such as. As lower alcohols or water can be removed. The addition of inert gas and the simultaneous removal of the more volatile components may be particularly advantageous when starting / starting the reaction, since by the addition of the reactants or by side reactions also inhibiting compounds can get into the reaction mixture.

As DMC catalyst, it is possible to use all known DMC catalysts, preferably those which contain zinc and cobalt, preferably those which contain 2-hexacyanocobaltate (III). Preferably, the in US 5,158,922 . US 20030119663 . WO 01/80994 or used in the above-mentioned writings DMC catalysts. The catalysts may be amorphous or crystalline. In the reaction mixture, the catalyst concentration is preferably> 0 to 1000 wppm (ppm by mass), preferably> 0 to 500 wppm, more preferably from 0.1 to 200 wppm and most preferably from 1 to 50 wppm. This concentration is based on the total mass of the resulting silicone polyether copolymer systems.

Preferably, the catalyst is dosed only once in the reactor. The amount of catalyst should be adjusted to provide sufficient catalytic activity for the process. The catalyst can be metered in as a solid or in the form of a catalyst suspension. If a suspension is used, in particular starters of the formulas (I) or (VII) or in the non-prepublished document are suitable DE 10 2008 002713.8 described polyether siloxanes as suspending agent. Preferably, however, waives a suspension.

By the method according to the invention high molecular weight, polyether-siloxane copolymer systems are provided, which are characterized in that they can be produced specifically and reproducibly in terms of structure and molecular weight. The sequence of the monomer units can be made variable within wide limits. Epoxide monomers of the type (II) and (III) and lactones of the formula (IV) can be randomly arranged in a row or randomly incorporated into the polymer chain. The fragments inserted into the resulting polymer chain by the reaction with ring opening of the reaction components of the formulas (II) to (VI) are freely permutatable with one another in their sequence, with the proviso that cyclic anhydrides according to formula (V) and (VI) and carbon dioxide are random inserted, so do not exist in homologous blocks, in the polyether structure.

In principle, all suitable reactor types can be used as reactors for the reaction claimed according to the invention, which can control the reaction and its possibly existing heat of reaction. The reaction can be carried out in a process-known manner continuously, semi-continuously or batchwise and can be flexibly adapted to the existing production equipment. In addition to conventional stirred tank reactors can also jet loop reactors with gas phase and internal heat exchanger tubes, as in WO 01/062826 described, are used. In addition, gas-phase-free loop reactors can be used.

In the dosage of the educts, a good distribution of the substances involved in the chemical reaction, i. the epoxide monomer, starter, DMC catalyst and optionally suspending agent or comonomers such as lactones, anhydrides or carbon dioxide necessary.

The invention further provides the silicone polyether copolymers prepared by the processes described, as well as plastic articles produced therefrom and the surfactant compositions containing silicone polyether copolymers, including the use thereof.

Further objects of the invention are described by the claims. The disclosure of the claims is in its entirety a part of the description.

The process according to the invention for the DMC-catalyzed alkoxylation of polyethersiloxanes with reactive hydrogen is described below by way of example, without the invention being deemed to be limited to these exemplary embodiments.
Given below, ranges, general formulas, or classes of compounds are intended to encompass not only the corresponding regions or groups of compounds explicitly mentioned, but also all sub-regions and sub-groups of compounds obtained by removing individual values (ranges) or compounds can be.

EXAMPLES

In the examples given below, the present invention is described by way of example, without the invention, the scope of application of which is apparent from the entire description and the claims, being limited to the embodiments mentioned in the examples.

OH numbers were analyzed by the standard acetylation method (phthalic anhydride). The GPC analyzes were carried out in THF as a solvent against polypropylene glycol as standard.

The polyethersiloxanes used as starting materials in Examples 1-3 and 5 and obtained by hydrosilylation reaction contain, as a result of the preparation, a proportion of excess polyether which is needed to complete the Si-H reaction. The proportion of co-used excess polyether is noted in the respective amounts of the examples.

Example 1:

As the chain initiator is a polyether of the formula (I) having the structure m ¹ = 20, m ² = 5, m ³ = m ⁴ = 0, X = X ¹ = methyl used previously by hydrosilylation of a hydrogen with an excess of OH -terminated allyl polyether of average molecular weight 800 g / mol and consisting of 36 wt .-% of ethylene oxide and 64 wt .-% of propylene oxide units, prepared according to the prior art.
200.0 g of this polyethersiloxane (containing 15-20% by weight of excess polyethers of average molecular weight 800 g / mol) and 0.10 g of zinc hexacyanocobaltate-DMC catalyst are placed under nitrogen in a 3 liter autoclave and heated to 130 with stirring ° C heated. The reactor is evacuated to an internal pressure of 30 mbar in order to remove any existing volatile constituents by distillation. To activate the DMC catalyst, a portion of 40.0 g of propylene oxide is fed. After 15 minutes and the reaction has started (the internal pressure drop in the reactor), a further 760.0 g of propylene oxide are continuously and with cooling within 2 hours at 130 ° C. and max. 0.6 bar absolute internal reactor pressure. The 30 minute post-reaction at 130 ° C is followed by the degassing stage. In this case, volatile components such as residual propylene oxide are distilled off in vacuo. The finished medium-viscosity and colorless polyethersiloxane copolymer is cooled to below 80 ° C and discharged from the reactor.
The product contains on average per polyethersiloxane molecule 5 long polyether chains, chemically bonded via a respective SiC bond to the siloxane skeleton, and has an OH number of 11.1 mg KOH / g. The GPC shows a multimodal curve with maxima at about 5,000, 9,000 and 20,000 g / mol, a weight average molecular weight M _w of 14,300 g / mol and a polydispersity M _w / M _n of 1.63.

Example 2:

1. a) 18 Gew.-% Ethylenoxid, 82 Gew.-% Propylenoxid, 1.400 g/mol, R¹³ in Formel (Ib) = Methyl,
2. b) 74 Gew.-% Ethylenoxid, 26 Gew.-% Propylenoxid, 3.800 g/mol, R¹³ in Formel (Ib) = Methyl,
3. c) 42 Gew.-% Ethylenoxid, 58 Gew.-% Propylenoxid, 3.800 g/mol

im Massenverhältnis 41:17:42.
In einem 3 Liter Autoklaven werden 162,0 g dieses Polyethersiloxans (enthaltend etwa 20 Gew.-% Überschuss-Polyethermischung) und 0,024 g Zinkhexacyanocobaltat-DMC-Katalysator unter Stickstoff vorgelegt und unter Rühren auf 130 °C aufgeheizt. Der Reaktor wird bis auf einen Innendruck von 30 mbar evakuiert, um evtl. vorhandene flüchtige Inhaltsstoffe destillativ zu entfernen. Zur Aktivierung des DMC-Katalysators wird eine Portion von 20,0 g Propylenoxid zugeführt. Nach 12 min und Anspringen der Reaktion werden weitere 62, 0 g Propylenoxid kontinuierlich und unter Kühlen innerhalb von 40 min bei 130 °C und max. 0,3 bar Reaktorinnendruck absolut zudosiert. Nach 40 min Nachreaktion bei 130 °C wird entgast. Dabei werden flüchtige Anteile wie restliches Propylenoxid im Vakuum abdestilliert. Das fertige mittelviskose und farblose Polyethersiloxan-Copolymere wird auf unter 80 °C abgekühlt und aus dem Reaktor abgelassen.
Das Produkt enthält im Mittel pro Polyethersiloxan-Molekül 6,5 lange Polyetherketten, chemisch über jeweils eine SiC-Bindung an das Siloxangerüst gebunden, und hat eine OH-Zahl von 4,9 mg KOH/g. Das GPC zeigt eine multimodale Kurve mit Maxima bei etwa 1.400, 9.000 und 20.000 g/mol, eine massenmittlere Molmasse M_w von 16.300 g/mol und eine Polydispersität M_w/M_n von 2,32.The chain starter is a hydrosilylated polyether siloxane of the structure m ¹ = 61.5; m ² = 1.6; m ³ = 4.9; m ⁴ = 0, X = X ¹ = methyl, using a mixture of a terminal OH-functional and two methyl-capped allyl polyethers whose composition is as follows:

1. a) 18% by weight of ethylene oxide, 82% by weight of propylene oxide, 1,400 g / mol, R ¹³ in formula (Ib) = methyl,
2. b) 74% by weight of ethylene oxide, 26% by weight of propylene oxide, 3,800 g / mol, R ¹³ in formula (Ib) = methyl,
3. c) 42% by weight of ethylene oxide, 58% by weight of propylene oxide, 3800 g / mol

in mass ratio 41:17:42.
In a 3 liter autoclave, 162.0 g of this polyethersiloxane (containing about 20 wt .-% excess polyether mixture) and 0.024 g of zinc hexacyanocobaltate DMC catalyst are placed under nitrogen and heated to 130 ° C with stirring. The reactor is evacuated to an internal pressure of 30 mbar in order to remove any existing volatile constituents by distillation. To activate the DMC catalyst, a portion of 20.0 g of propylene oxide is fed. After 12 minutes and starting the reaction, a further 62.0 g of propylene oxide are continuously and with cooling within 40 min at 130 ° C and max. 0.3 bar absolute internal pressure of the reactor. After 40 minutes post-reaction at 130 ° C is degassed. In this case, volatile components such as residual Distilled off propylene oxide in vacuo. The finished medium-viscosity and colorless polyethersiloxane copolymer is cooled to below 80 ° C and discharged from the reactor.
The product contains on average per polyethersiloxane molecule 6.5 long polyether chains, chemically bonded via a respective SiC bond to the siloxane skeleton, and has an OH number of 4.9 mg KOH / g. The GPC shows a multimodal curve with maxima at about 1,400, 9,000 and 20,000 g / mol, a weight-average molecular weight M _w of 16,300 g / mol and a polydispersity M _w / M _n of 2.32.

Example 3:

1. a) 10 Gew.-% Ethylenoxid, 90 Gew.-% Propylenoxid, 1.500 g/mol,
2. b) 58 Gew.-% Ethylenoxid, 42 Gew.-% Propylenoxid, 1.300 g/mol,
3. c) 42 Gew.-% Ethylenoxid, 58 Gew.-% Propylenoxid, 3.800 g/mol

im Massenverhältnis 36:6:58.
In einem 3 Liter Autoklaven werden 159,0 g dieses Polyethersiloxans (enthaltend etwa 20 Gew.-% Überschuss-Polyethermischung) und 0,031 g Zinkhexacyanocobaltat-DMC-Katalysator unter Stickstoff vorgelegt und unter Rühren auf 130 °C aufgeheizt. Der Reaktor wird bis auf einen Innendruck von 30 mbar evakuiert, um evtl. vorhandene flüchtige Inhaltsstoffe destillativ zu entfernen. Zur Aktivierung des DMC-Katalysators wird eine Portion von 21,0 g Propylenoxid zugeführt. Nach 12 min und Anspringen der Reaktion werden weitere 177,0 g Propylenoxid kontinuierlich und unter Kühlen innerhalb von 45 min bei 130 °C und max. 0,5 bar Reaktorinnendruck absolut zudosiert. Nach 35 min Nachreaktion bei 130 °C wird entgast. Dabei werden flüchtige Anteile wie restliches Propylenoxid im Vakuum abdestilliert. Das fertige mittelviskose und farblose Polyethersiloxan-Copolymere wird auf unter 80 °C abgekühlt und aus dem Reaktor abgelassen.
Das Produkt enthält im Mittel pro Polyethersiloxan-Molekül 6,5 lange Polyetherketten, chemisch über jeweils eine SiC-Bindung an das Siloxangerüst gebunden, und hat eine OH-Zahl von 10,8 mg KOH/g. Das GPC zeigt eine bimodale Kurve mit Maxima bei etwa 8.000 und 30.000 g/mol, eine massenmittlere Molmasse M_w von 8.600 g/mol und eine Polydispersität M_w/M_n von 2,36.The chain starter is a hydrosilylated polyether siloxane of the structure m ¹ = 61.5; m ² = 6.5; m ³ = m ⁴ = 0, X = X ¹ = methyl, using a mixture of three terminal OH-functional allyl polyethers whose composition is as follows:

1. a) 10% by weight of ethylene oxide, 90% by weight of propylene oxide, 1500 g / mol,
2. b) 58% by weight of ethylene oxide, 42% by weight of propylene oxide, 1300 g / mol,
3. c) 42% by weight of ethylene oxide, 58% by weight of propylene oxide, 3800 g / mol

in a mass ratio of 36: 6: 58.
In a 3 liter autoclave 159.0 g of this polyethersiloxane (containing about 20 wt .-% excess polyether mixture) and 0.031 g of zinc hexacyanocobaltate DMC catalyst are placed under nitrogen and heated to 130 ° C with stirring. The reactor is evacuated to an internal pressure of 30 mbar in order to remove any existing volatile constituents by distillation. to Activation of the DMC catalyst is fed to a portion of 21.0 g of propylene oxide. After 12 minutes and starting the reaction, a further 177.0 g of propylene oxide are continuously and with cooling within 45 min at 130 ° C and max. 0.5 bar internal reactor pressure metered absolutely. After 35 min post-reaction at 130 ° C is degassed. In this case, volatile components such as residual propylene oxide are distilled off in vacuo. The finished medium-viscosity and colorless polyethersiloxane copolymer is cooled to below 80 ° C and discharged from the reactor.
The product contains on average per polyethersiloxane molecule 6.5 long polyether chains, chemically bonded via a respective SiC bond to the siloxane skeleton, and has an OH number of 10.8 mg KOH / g. The GPC shows a bimodal curve with maxima at about 8,000 and 30,000 g / mol, a weight average molecular weight M _w of 8,600 g / mol and a polydispersity M _w / M _n of 2.36.

Example 4:

The chain starter used is a linear polyethersiloxane which was previously prepared by propoxylating an α, ω-dihydroxypolydimethylsiloxane having an average chain length of 51 Si (CH ₃ ) ₂ O units, and whose two OH-terminated polyether chains have an average molecular weight of approx. 600 g / mol.
250.0 g of this polyethersiloxane and 0.023 g of zinc hexacyanocobaltate-DMC catalyst are placed under nitrogen in a 3 liter autoclave and heated to 130 ° C. with stirring. The reactor is evacuated to an internal pressure of 30 mbar in order to remove any existing volatile constituents by distillation. To activate the DMC catalyst, a portion of 36.0 g of propylene oxide supplied. After 15 minutes and starting the reaction, a further 485.0 g of propylene oxide are continuously and with cooling within 1.5 h at 130 ° C and max. 0.5 bar internal reactor pressure metered absolutely. The 30 minute post-reaction at 130 ° C is followed by the degassing stage. In this case, volatile components such as residual propylene oxide are distilled off in vacuo. The finished medium-viscosity and slightly cloudy polyethersiloxane copolymer is cooled to below 80 ° C and discharged from the reactor.
The product contains on average per polyethersiloxane molecule 2 long terminal polyether chains, chemically bonded via a respective SiOC bond to the siloxane skeleton, and has an OH number of 7.2 mg KOH / g. The GPC shows a maximum at about 15,000 g / mol and a polydispersity M _w / M _n of 1.42.

Example 5:

As the chain initiator is a polyether of the formula (I) having the structure m ¹ = 42, m ² = 6, m ³ = m ⁴ = 0, X = X ¹ = methyl employed which previously a by hydrosilylation of the corresponding hydrosiloxane with an excess OH-terminated allyl polyether of average molecular weight 600 g / mol and consisting of 50 wt .-% of ethylene oxide and 50 wt .-% of propylene oxide units, was prepared according to the prior art.
In a 3 liter autoclave, 150.0 g of this polyethersiloxane (containing 15-20 wt .-% excess polyethers of average molecular weight 600 g / mol) and 0.16 g of zinc hexacyanocobaltate DMC catalyst are placed under nitrogen and with stirring to 130 ° C heated. The reactor is up to an internal pressure of 30 mbar evacuated to remove any existing volatile constituents by distillation. To activate the DMC catalyst, a portion of 40.0 g of propylene oxide is fed. After 15 minutes and starting the reaction, a further 296 g of propylene oxide (sampling, product 1), then a further 2,250 g of propylene oxide continuously and under cooling within 3.45 h at 130 ° C and max. 0.6 bar absolute internal reactor pressure. The 30 minute post-reaction at 130 ° C is followed by the degassing stage. In this case, volatile components such as residual propylene oxide are distilled off in vacuo. The finished medium-viscosity and yellowish polyethersiloxane copolymer (product 2) is cooled to below 80 ° C and discharged from the reactor.
The product has an OH number of 4.2 mg KOH / g. The GPC ( Fig. 1 ) shows a multimodal curve whose maxima shift continuously in the course of the alkoxylation reaction to higher molecular weights. The weight average molecular weight M _{w of} the end product (product 2) is 35,450 g / mol, the polydispersity M _w / M _n of 1.6.
The Fig. 1 shows the change in GPC analysis over the course of the reaction. All peak maxima migrate along the X axis to higher average molecular weights. A preference for the alkoxylation according to catch-up kinetics, as would have been expected for the short-chain polyetherols is not apparent. On the "adulteration" due to the GPC analyzes standardized logarithmic representation of the molecular weight scale is only marginally noted.

Claims (14)

Process for the alkoxylation of silicone polyether copolymers, characterized in that double metal cyanide catalysts are used. A process according to claim 1 for the alkoxylation of compositions comprising silicone polyether copolymers to double metal cyanide catalysts, characterized in that silicone polyether copolymer compositions are formed with an increased average molecular weight compared to the educts. Process for the preferred alkoxylation of silicone polyether copolymers in compositions comprising free polyetherols to double metal cyanide catalysts , characterized in that the structure of the average molecular weight of the silicone polyether used in admixture with free polyetherol at least at the same speed as the structure of the molecular weight of the present in the reactant mixture free polyetherol. A process for the preferred alkoxylation of silicone polyether copolymers in compositions containing free polyetherols on double metal cyanide catalysts, characterized in that the construction of the average molecular weight of the silicone polyether copolymer used in admixture with free polyetherol at least with the same probability of reaction takes place as the structure of the molecular weight of the free polyetherol present in the starting material mixture. A method according to claim 3, characterized in that the structure of the molecular weight of the silicone polyether copolymers is faster than the structure of the molecular weight of the polyether polyol. Process according to at least one of Claims 1 to 5, characterized in that the silicone polyether copolymers produced are relatively high molecular mass, alkoxy silicone polyether copolymers having complex compositions, hydrophobic and hydrophilic structural elements. Process according to at least one of Claims 1 to 6, characterized in that the alkoxylation reaction is a ring-opening alkoxylation reaction on double metal cyanide catalysts. Process according to at least one of claims 3, 5 or 7, characterized in that the rate of alkoxylation for all of the reacting silicone polyether copolymers is greater than or equal to the rate of alkoxylation of the polyetherol. A method according to any one of claims 1 to 8, characterized in that SiC-linked silicone polyether copolymers of different structure, molecular weight and molecular weight distribution, the have at least one reactive carbon-bonded hydroxyl group, be reacted in the presence of a double metal cyanide catalyst with epoxy monomers and optionally other monomers to chain extended, modified silicone polyether copolymers. Process for the preparation of alkoxylation products containing silicone polyether copolymers according to at least one of Claims 1 to 9 by means of double metal cyanide catalysis, in which one or more epoxide-functional monomers of the formula (II)

in which R ² or R ^3, and R ⁵ or R ⁶ can be H or a saturated or optionally mono- or polyunsaturated, including further substituted, optionally mono- or polyvalent hydrocarbon radical equal to, or independently of one another, wherein the radicals R ⁵ or R ⁶ is that they are equal to a monovalent hydrocarbon radical and the hydrocarbon radical may be cycloaliphatically bridged via the fragment Y and Y may not be present, or a methylene bridge with May be 1 or 2 methylene units, individually or in admixture with further epoxide compounds and optionally further comonomers such as lactones cyclic anhydrides, carbon dioxide or oxetanes optionally blockwise or randomly to a silicone polyether copolymer of the formulas (I)

or (VII)

be added with at least one reactive hydrogen, wherein m ^{1 is} an integer from 0 to 500, m ^{2 is} an integer from 0 to 60, m ^{3 is} an integer from 0 to 60, m ^{4 is} an integer from 0 to 10, is X is a linear, cyclic or branched, aliphatic or aromatic, saturated or unsaturated hydrocarbon radical having 1 to 20 C atoms, which may optionally contain heteroatoms such as oxygen, nitrogen, phosphorus or sulfur, but which is preferably a methyl group, X ^{1 is} optionally X, X ² or X ³ , X ^{2 is} an OH-functional, optionally ester or carbonate-modified polyoxyalkylene radical of the formula (Ia),

X ^{3 is} a terminally etherified polyoxyalkylene radical of the formula (Ib),

or a terminally esterified with a monofunctional carboxylic acid polyoxyalkylene radical of the formula (Ic)

in which R ⁴ corresponds to a linear or branched alkyl radical of 1 to 24 carbon atoms which is bonded to an aromatic or cycloaliphatic radical, R ⁷ and R ^{8 are} independently either hydrogen, alkyl, alkoxy, aryl or aralkyl groups, as well as R ^9, R ^10, R ¹¹ and R ¹² are independently either hydrogen, alkyl, alkenyl, alkoxy, aryl or aralkyl and the hydrocarbon radical may be bridged cycloaliphatic or aromatic, via the fragment Z, wherein Z is either a divalent alkylene also represent alkenylene radical and R ^{13 is} optionally an alkyl group having 1 to 18 C atoms, preferably methyl, wherein R ^{14 is} a saturated or a mono- or polyunsaturated, either linear or branched, aliphatic or aromatic hydrocarbon radical having 1-30 carbon atoms, which in turn can carry OH groups, and which is preferably a methyl radical, and wherein c is an integer from 0 to 24, e is an integer greater than or equal to 5, and f, g, h, i and j are integers from 0 to 500. Silicone polyether copolymers and their compositions, prepared by one of the processes according to claims 1 to 10. A surfactant composition containing silicone polyether copolymers prepared by any of the processes according to claims 1 to 10. Plastic article comprising silicone polyether copolymers prepared by one of the processes according to claims 1 to 10. Use of the alkoxylated compounds prepared by one of the processes according to claims 1 to 10, optionally further functionalized silicone polyether copolymers as surfactants.

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